- InChI
- InChI=1S/C6H12O6/c7-2-6(11)5(10)4(9)3(8)1-12-6/h3-5,7-11H,1-2H2
- InChI Key
- LKDRXBCSQODPBY-UHFFFAOYSA-N
- Formula
- C6H12O6
- SMILES
- OCC1(O)OCC(O)C(O)C1O
- Molecular Weight1
- 180.16
- CAS
- 6347-01-9
- Other Names
-
- D-(-)-fructose
- levulose
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | -2809.80 | kJ/mol | NIST |
| ΔfG° | -774.75 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -1051.78 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 28.46 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 115.21 | kJ/mol | Joback Calculated Property |
| log10WS | 1.42 | Crippen Calculated Property | |
| logPoct/wat | -3.220 | Crippen Calculated Property | |
| McVol | 119.760 | ml/mol | McGowan Calculated Property |
| Pc | 7037.97 | kPa | Joback Calculated Property |
| Tboil | 830.31 | K | Joback Calculated Property |
| Tc | 1017.85 | K | Joback Calculated Property |
| Tfus | 506.61 | K | Joback Calculated Property |
| Vc | 0.415 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [409.17; 458.97] | J/mol×K | [830.31; 1017.85] | 
|
|
T(K) Ideal gas heat capacity (J/mol×K) 410 420 430 440 450 460 850 900 950 1000 | ||||
| Cp,gas | 409.17 | J/mol×K | 830.31 | Joback Calculated Property |
| Cp,gas | 417.53 | J/mol×K | 861.57 | Joback Calculated Property |
| Cp,gas | 425.78 | J/mol×K | 892.82 | Joback Calculated Property |
| Cp,gas | 434.00 | J/mol×K | 924.08 | Joback Calculated Property |
| Cp,gas | 442.23 | J/mol×K | 955.34 | Joback Calculated Property |
| Cp,gas | 450.53 | J/mol×K | 986.59 | Joback Calculated Property |
| Cp,gas | 458.97 | J/mol×K | 1017.85 | Joback Calculated Property |
| Cp,solid | [2.81; 290.40] | J/mol×K | [14.06; 370.00] |
|
|
T(K) Solid phase heat capacity (J/mol×K) 0 50 100 150 200 250 300 100 200 300 | ||||
| Cp,solid | 2.81 | J/mol×K | 14.06 | Heat ca... |
| Cp,solid | 3.13 | J/mol×K | 14.48 | Heat ca... |
| Cp,solid | 3.38 | J/mol×K | 14.92 | Heat ca... |
| Cp,solid | 6.23 | J/mol×K | 15.00 | Apparen... |
| Cp,solid | 3.63 | J/mol×K | 15.36 | Heat ca... |
| Cp,solid | 3.92 | J/mol×K | 15.81 | Heat ca... |
| Cp,solid | 4.22 | J/mol×K | 16.27 | Heat ca... |
| Cp,solid | 4.66 | J/mol×K | 16.77 | Heat ca... |
| Cp,solid | 5.05 | J/mol×K | 17.29 | Heat ca... |
| Cp,solid | 5.33 | J/mol×K | 17.75 | Heat ca... |
| Cp,solid | 5.75 | J/mol×K | 18.24 | Heat ca... |
| Cp,solid | 6.19 | J/mol×K | 18.76 | Heat ca... |
| Cp,solid | 6.58 | J/mol×K | 19.31 | Heat ca... |
| Cp,solid | 7.07 | J/mol×K | 19.89 | Heat ca... |
| Cp,solid | 9.95 | J/mol×K | 20.00 | Apparen... |
| Cp,solid | 7.63 | J/mol×K | 20.47 | Heat ca... |
| Cp,solid | 8.08 | J/mol×K | 21.03 | Heat ca... |
| Cp,solid | 8.51 | J/mol×K | 21.55 | Heat ca... |
| Cp,solid | 9.02 | J/mol×K | 22.09 | Heat ca... |
| Cp,solid | 9.57 | J/mol×K | 22.64 | Heat ca... |
| Cp,solid | 10.10 | J/mol×K | 23.22 | Heat ca... |
| Cp,solid | 10.61 | J/mol×K | 23.84 | Heat ca... |
| Cp,solid | 11.21 | J/mol×K | 24.41 | Heat ca... |
| Cp,solid | 11.67 | J/mol×K | 24.96 | Heat ca... |
| Cp,solid | 13.13 | J/mol×K | 25.00 | Apparen... |
| Cp,solid | 12.67 | J/mol×K | 25.84 | Heat ca... |
| Cp,solid | 13.50 | J/mol×K | 26.71 | Heat ca... |
| Cp,solid | 14.07 | J/mol×K | 27.31 | Heat ca... |
| Cp,solid | 14.91 | J/mol×K | 28.19 | Heat ca... |
| Cp,solid | 15.70 | J/mol×K | 29.03 | Heat ca... |
| Cp,solid | 16.16 | J/mol×K | 29.58 | Heat ca... |
| Cp,solid | 15.91 | J/mol×K | 30.00 | Apparen... |
| Cp,solid | 16.84 | J/mol×K | 30.14 | Heat ca... |
| Cp,solid | 17.43 | J/mol×K | 30.73 | Heat ca... |
| Cp,solid | 18.05 | J/mol×K | 31.35 | Heat ca... |
| Cp,solid | 18.53 | J/mol×K | 31.98 | Heat ca... |
| Cp,solid | 19.19 | J/mol×K | 32.62 | Heat ca... |
| Cp,solid | 19.89 | J/mol×K | 33.28 | Heat ca... |
| Cp,solid | 20.59 | J/mol×K | 33.96 | Heat ca... |
| Cp,solid | 21.26 | J/mol×K | 34.65 | Heat ca... |
| Cp,solid | 18.49 | J/mol×K | 35.00 | Apparen... |
| Cp,solid | 21.95 | J/mol×K | 35.36 | Heat ca... |
| Cp,solid | 22.67 | J/mol×K | 36.07 | Heat ca... |
| Cp,solid | 23.42 | J/mol×K | 36.78 | Heat ca... |
| Cp,solid | 24.11 | J/mol×K | 37.50 | Heat ca... |
| Cp,solid | 24.83 | J/mol×K | 38.21 | Heat ca... |
| Cp,solid | 25.52 | J/mol×K | 38.91 | Heat ca... |
| Cp,solid | 26.21 | J/mol×K | 39.60 | Heat ca... |
| Cp,solid | 20.98 | J/mol×K | 40.00 | Apparen... |
| Cp,solid | 26.89 | J/mol×K | 40.28 | Heat ca... |
| Cp,solid | 27.59 | J/mol×K | 40.99 | Heat ca... |
| Cp,solid | 28.30 | J/mol×K | 41.73 | Heat ca... |
| Cp,solid | 29.02 | J/mol×K | 42.48 | Heat ca... |
| Cp,solid | 29.78 | J/mol×K | 43.26 | Heat ca... |
| Cp,solid | 30.54 | J/mol×K | 44.03 | Heat ca... |
| Cp,solid | 31.29 | J/mol×K | 44.80 | Heat ca... |
| Cp,solid | 23.44 | J/mol×K | 45.00 | Apparen... |
| Cp,solid | 32.07 | J/mol×K | 45.60 | Heat ca... |
| Cp,solid | 32.85 | J/mol×K | 46.41 | Heat ca... |
| Cp,solid | 33.62 | J/mol×K | 47.23 | Heat ca... |
| Cp,solid | 34.43 | J/mol×K | 48.05 | Heat ca... |
| Cp,solid | 35.18 | J/mol×K | 48.87 | Heat ca... |
| Cp,solid | 35.98 | J/mol×K | 49.66 | Heat ca... |
| Cp,solid | 25.91 | J/mol×K | 50.00 | Apparen... |
| Cp,solid | 36.72 | J/mol×K | 50.46 | Heat ca... |
| Cp,solid | 37.50 | J/mol×K | 51.30 | Heat ca... |
| Cp,solid | 38.33 | J/mol×K | 52.17 | Heat ca... |
| Cp,solid | 39.16 | J/mol×K | 53.08 | Heat ca... |
| Cp,solid | 40.03 | J/mol×K | 54.00 | Heat ca... |
| Cp,solid | 40.88 | J/mol×K | 54.92 | Heat ca... |
| Cp,solid | 41.75 | J/mol×K | 55.87 | Heat ca... |
| Cp,solid | 42.65 | J/mol×K | 56.84 | Heat ca... |
| Cp,solid | 43.54 | J/mol×K | 57.80 | Heat ca... |
| Cp,solid | 44.39 | J/mol×K | 58.75 | Heat ca... |
| Cp,solid | 45.25 | J/mol×K | 59.68 | Heat ca... |
| Cp,solid | 46.09 | J/mol×K | 60.61 | Heat ca... |
| Cp,solid | 46.94 | J/mol×K | 61.55 | Heat ca... |
| Cp,solid | 47.76 | J/mol×K | 62.48 | Heat ca... |
| Cp,solid | 48.61 | J/mol×K | 63.40 | Heat ca... |
| Cp,solid | 49.43 | J/mol×K | 64.31 | Heat ca... |
| Cp,solid | 50.22 | J/mol×K | 65.22 | Heat ca... |
| Cp,solid | 51.08 | J/mol×K | 66.18 | Heat ca... |
| Cp,solid | 51.94 | J/mol×K | 67.16 | Heat ca... |
| Cp,solid | 52.90 | J/mol×K | 68.22 | Heat ca... |
| Cp,solid | 53.88 | J/mol×K | 69.33 | Heat ca... |
| Cp,solid | 54.83 | J/mol×K | 70.43 | Heat ca... |
| Cp,solid | 55.79 | J/mol×K | 71.50 | Heat ca... |
| Cp,solid | 56.77 | J/mol×K | 72.63 | Heat ca... |
| Cp,solid | 57.78 | J/mol×K | 73.81 | Heat ca... |
| Cp,solid | 58.80 | J/mol×K | 74.97 | Heat ca... |
| Cp,solid | 59.77 | J/mol×K | 76.11 | Heat ca... |
| Cp,solid | 60.74 | J/mol×K | 77.23 | Heat ca... |
| Cp,solid | 61.72 | J/mol×K | 78.40 | Heat ca... |
| Cp,solid | 62.76 | J/mol×K | 79.61 | Heat ca... |
| Cp,solid | 63.77 | J/mol×K | 80.81 | Heat ca... |
| Cp,solid | 64.80 | J/mol×K | 81.98 | Heat ca... |
| Cp,solid | 65.76 | J/mol×K | 83.14 | Heat ca... |
| Cp,solid | 66.77 | J/mol×K | 84.34 | Heat ca... |
| Cp,solid | 67.84 | J/mol×K | 85.59 | Heat ca... |
| Cp,solid | 68.83 | J/mol×K | 86.82 | Heat ca... |
| Cp,solid | 69.88 | J/mol×K | 88.03 | Heat ca... |
| Cp,solid | 70.89 | J/mol×K | 89.22 | Heat ca... |
| Cp,solid | 71.89 | J/mol×K | 90.46 | Heat ca... |
| Cp,solid | 72.99 | J/mol×K | 91.74 | Heat ca... |
| Cp,solid | 73.99 | J/mol×K | 93.00 | Heat ca... |
| Cp,solid | 75.03 | J/mol×K | 94.24 | Heat ca... |
| Cp,solid | 76.03 | J/mol×K | 95.47 | Heat ca... |
| Cp,solid | 77.10 | J/mol×K | 96.74 | Heat ca... |
| Cp,solid | 78.13 | J/mol×K | 98.05 | Heat ca... |
| Cp,solid | 79.20 | J/mol×K | 99.34 | Heat ca... |
| Cp,solid | 54.01 | J/mol×K | 100.00 | Apparen... |
| Cp,solid | 80.23 | J/mol×K | 100.61 | Heat ca... |
| Cp,solid | 81.25 | J/mol×K | 101.88 | Heat ca... |
| Cp,solid | 82.30 | J/mol×K | 103.17 | Heat ca... |
| Cp,solid | 83.38 | J/mol×K | 104.51 | Heat ca... |
| Cp,solid | 84.42 | J/mol×K | 105.83 | Heat ca... |
| Cp,solid | 85.50 | J/mol×K | 107.14 | Heat ca... |
| Cp,solid | 86.51 | J/mol×K | 108.44 | Heat ca... |
| Cp,solid | 87.55 | J/mol×K | 109.77 | Heat ca... |
| Cp,solid | 88.69 | J/mol×K | 111.13 | Heat ca... |
| Cp,solid | 89.72 | J/mol×K | 112.49 | Heat ca... |
| Cp,solid | 90.79 | J/mol×K | 113.83 | Heat ca... |
| Cp,solid | 91.82 | J/mol×K | 115.15 | Heat ca... |
| Cp,solid | 92.94 | J/mol×K | 116.54 | Heat ca... |
| Cp,solid | 94.07 | J/mol×K | 118.00 | Heat ca... |
| Cp,solid | 95.21 | J/mol×K | 119.43 | Heat ca... |
| Cp,solid | 96.29 | J/mol×K | 120.86 | Heat ca... |
| Cp,solid | 97.42 | J/mol×K | 122.27 | Heat ca... |
| Cp,solid | 98.53 | J/mol×K | 123.72 | Heat ca... |
| Cp,solid | 99.73 | J/mol×K | 125.19 | Heat ca... |
| Cp,solid | 100.86 | J/mol×K | 126.66 | Heat ca... |
| Cp,solid | 101.99 | J/mol×K | 128.15 | Heat ca... |
| Cp,solid | 103.12 | J/mol×K | 129.65 | Heat ca... |
| Cp,solid | 104.32 | J/mol×K | 131.18 | Heat ca... |
| Cp,solid | 105.56 | J/mol×K | 132.78 | Heat ca... |
| Cp,solid | 106.79 | J/mol×K | 134.41 | Heat ca... |
| Cp,solid | 107.97 | J/mol×K | 136.01 | Heat ca... |
| Cp,solid | 109.25 | J/mol×K | 137.61 | Heat ca... |
| Cp,solid | 110.50 | J/mol×K | 139.24 | Heat ca... |
| Cp,solid | 111.75 | J/mol×K | 140.90 | Heat ca... |
| Cp,solid | 112.96 | J/mol×K | 142.55 | Heat ca... |
| Cp,solid | 114.21 | J/mol×K | 144.18 | Heat ca... |
| Cp,solid | 115.47 | J/mol×K | 145.81 | Heat ca... |
| Cp,solid | 116.73 | J/mol×K | 147.46 | Heat ca... |
| Cp,solid | 117.96 | J/mol×K | 149.19 | Heat ca... |
| Cp,solid | 92.31 | J/mol×K | 150.00 | Apparen... |
| Cp,solid | 119.30 | J/mol×K | 150.94 | Heat ca... |
| Cp,solid | 120.61 | J/mol×K | 152.67 | Heat ca... |
| Cp,solid | 121.92 | J/mol×K | 154.39 | Heat ca... |
| Cp,solid | 123.22 | J/mol×K | 156.15 | Heat ca... |
| Cp,solid | 124.55 | J/mol×K | 157.94 | Heat ca... |
| Cp,solid | 125.90 | J/mol×K | 159.71 | Heat ca... |
| Cp,solid | 127.16 | J/mol×K | 161.48 | Heat ca... |
| Cp,solid | 128.53 | J/mol×K | 163.23 | Heat ca... |
| Cp,solid | 129.85 | J/mol×K | 165.01 | Heat ca... |
| Cp,solid | 131.22 | J/mol×K | 166.83 | Heat ca... |
| Cp,solid | 132.53 | J/mol×K | 168.63 | Heat ca... |
| Cp,solid | 133.87 | J/mol×K | 170.42 | Heat ca... |
| Cp,solid | 135.21 | J/mol×K | 172.26 | Heat ca... |
| Cp,solid | 136.66 | J/mol×K | 174.19 | Heat ca... |
| Cp,solid | 138.12 | J/mol×K | 176.16 | Heat ca... |
| Cp,solid | 139.54 | J/mol×K | 178.11 | Heat ca... |
| Cp,solid | 140.98 | J/mol×K | 180.05 | Heat ca... |
| Cp,solid | 142.44 | J/mol×K | 181.97 | Heat ca... |
| Cp,solid | 143.86 | J/mol×K | 183.93 | Heat ca... |
| Cp,solid | 145.37 | J/mol×K | 185.92 | Heat ca... |
| Cp,solid | 146.78 | J/mol×K | 187.90 | Heat ca... |
| Cp,solid | 148.24 | J/mol×K | 189.86 | Heat ca... |
| Cp,solid | 149.62 | J/mol×K | 191.82 | Heat ca... |
| Cp,solid | 151.13 | J/mol×K | 193.80 | Heat ca... |
| Cp,solid | 152.65 | J/mol×K | 195.89 | Heat ca... |
| Cp,solid | 154.23 | J/mol×K | 198.03 | Heat ca... |
| Cp,solid | 134.39 | J/mol×K | 200.00 | Apparen... |
| Cp,solid | 155.79 | J/mol×K | 200.16 | Heat ca... |
| Cp,solid | 157.38 | J/mol×K | 202.27 | Heat ca... |
| Cp,solid | 158.97 | J/mol×K | 204.41 | Heat ca... |
| Cp,solid | 160.59 | J/mol×K | 206.59 | Heat ca... |
| Cp,solid | 162.27 | J/mol×K | 208.75 | Heat ca... |
| Cp,solid | 163.79 | J/mol×K | 210.91 | Heat ca... |
| Cp,solid | 165.43 | J/mol×K | 213.05 | Heat ca... |
| Cp,solid | 166.88 | J/mol×K | 215.22 | Heat ca... |
| Cp,solid | 168.61 | J/mol×K | 217.41 | Heat ca... |
| Cp,solid | 170.28 | J/mol×K | 219.60 | Heat ca... |
| Cp,solid | 172.01 | J/mol×K | 221.78 | Heat ca... |
| Cp,solid | 173.59 | J/mol×K | 223.94 | Heat ca... |
| Cp,solid | 175.10 | J/mol×K | 226.14 | Heat ca... |
| Cp,solid | 176.89 | J/mol×K | 228.44 | Heat ca... |
| Cp,solid | 178.65 | J/mol×K | 230.80 | Heat ca... |
| Cp,solid | 180.52 | J/mol×K | 233.16 | Heat ca... |
| Cp,solid | 182.33 | J/mol×K | 235.50 | Heat ca... |
| Cp,solid | 184.07 | J/mol×K | 237.87 | Heat ca... |
| Cp,solid | 185.87 | J/mol×K | 240.27 | Heat ca... |
| Cp,solid | 187.70 | J/mol×K | 242.65 | Heat ca... |
| Cp,solid | 189.43 | J/mol×K | 245.03 | Heat ca... |
| Cp,solid | 191.32 | J/mol×K | 247.39 | Heat ca... |
| Cp,solid | 193.01 | J/mol×K | 249.78 | Heat ca... |
| Cp,solid | 175.41 | J/mol×K | 250.00 | Apparen... |
| Cp,solid | 194.95 | J/mol×K | 252.20 | Heat ca... |
| Cp,solid | 196.74 | J/mol×K | 254.60 | Heat ca... |
| Cp,solid | 198.58 | J/mol×K | 257.00 | Heat ca... |
| Cp,solid | 200.50 | J/mol×K | 259.38 | Heat ca... |
| Cp,solid | 202.31 | J/mol×K | 261.79 | Heat ca... |
| Cp,solid | 204.15 | J/mol×K | 264.29 | Heat ca... |
| Cp,solid | 206.25 | J/mol×K | 266.82 | Heat ca... |
| Cp,solid | 208.09 | J/mol×K | 269.35 | Heat ca... |
| Cp,solid | 210.03 | J/mol×K | 271.87 | Heat ca... |
| Cp,solid | 211.71 | J/mol×K | 274.41 | Heat ca... |
| Cp,solid | 213.84 | J/mol×K | 276.98 | Heat ca... |
| Cp,solid | 215.75 | J/mol×K | 279.54 | Heat ca... |
| Cp,solid | 217.72 | J/mol×K | 282.08 | Heat ca... |
| Cp,solid | 219.77 | J/mol×K | 284.61 | Heat ca... |
| Cp,solid | 221.78 | J/mol×K | 287.17 | Heat ca... |
| Cp,solid | 220.30 | J/mol×K | 288.15 | Tempera... |
| Cp,solid | 223.86 | J/mol×K | 289.76 | Heat ca... |
| Cp,solid | 225.93 | J/mol×K | 292.33 | Heat ca... |
| Cp,solid | 223.60 | J/mol×K | 293.15 | Tempera... |
| Cp,solid | 227.98 | J/mol×K | 294.92 | Heat ca... |
| Cp,solid | 230.08 | J/mol×K | 297.52 | Heat ca... |
| Cp,solid | 227.70 | J/mol×K | 298.15 | Tempera... |
| Cp,solid | 214.57 | J/mol×K | 300.00 | Apparen... |
| Cp,solid | 232.18 | J/mol×K | 300.15 | Heat ca... |
| Cp,solid | 234.38 | J/mol×K | 302.81 | Heat ca... |
| Cp,solid | 233.30 | J/mol×K | 303.15 | Tempera... |
| Cp,solid | 236.46 | J/mol×K | 305.45 | Heat ca... |
| Cp,solid | 238.40 | J/mol×K | 308.08 | Heat ca... |
| Cp,solid | 236.90 | J/mol×K | 308.15 | Tempera... |
| Cp,solid | 240.73 | J/mol×K | 310.70 | Heat ca... |
| Cp,solid | 242.40 | J/mol×K | 313.15 | Tempera... |
| Cp,solid | 242.98 | J/mol×K | 313.34 | Heat ca... |
| Cp,solid | 244.99 | J/mol×K | 316.00 | Heat ca... |
| Cp,solid | 247.30 | J/mol×K | 318.15 | Tempera... |
| Cp,solid | 247.19 | J/mol×K | 318.66 | Heat ca... |
| Cp,solid | 249.35 | J/mol×K | 321.30 | Heat ca... |
| Cp,solid | 251.50 | J/mol×K | 323.15 | Tempera... |
| Cp,solid | 251.32 | J/mol×K | 323.93 | Heat ca... |
| Cp,solid | 253.53 | J/mol×K | 326.58 | Heat ca... |
| Cp,solid | 251.80 | J/mol×K | 328.15 | Tempera... |
| Cp,solid | 255.90 | J/mol×K | 329.26 | Heat ca... |
| Cp,solid | 255.10 | J/mol×K | 333.15 | Tempera... |
| Cp,solid | 259.60 | J/mol×K | 338.15 | Tempera... |
| Cp,solid | 260.90 | J/mol×K | 343.15 | Tempera... |
| Cp,solid | 266.40 | J/mol×K | 348.15 | Tempera... |
| Cp,solid | 251.78 | J/mol×K | 350.00 | Apparen... |
| Cp,solid | 275.30 | J/mol×K | 353.15 | Tempera... |
| Cp,solid | 290.40 | J/mol×K | 358.15 | Tempera... |
| Cp,solid | 265.80 | J/mol×K | 370.00 | Apparen... |
Similar Compounds
Find more compounds similar to D-Fructose.
Mixtures
- D-Fructose + Ethanol + Water
- D-Fructose + Water
- D-Fructose + Potassium phosphate, monobasic + Water
- D-Fructose + D-Alanine + Water
- D-Fructose + D-Valine + Water
- D-Fructose + D-Leucine + Water
- D-Fructose + Urea + Water
- D-Fructose + Choline chloride
- potassium chloride + D-Fructose + Water
- D-Fructose + Water + Acetic acid, sodium salt, hydrate (1:1:3)
- Magnesium chloride + D-Fructose + Water
- D-Fructose + dl-Alanine + Water
- D-Fructose + Water + Potassium oxalate
- D-Fructose + Water + 1,4,7,10,13,16-Hexaoxacyclooctadecane
- D-Fructose + Water + N-(N-Glycylglycyl)glycine
- D-Fructose + Glycine, N-acetyl- + Water
- D-Fructose + 1H-Imidazole + Acetic acid
- Betaine + Pentanoic acid, 4-oxo- + D-Fructose
- D-Fructose + Choline chloride + Urea
- D-Fructose + Choline chloride + 1,2-Ethanediol
Find more mixtures with D-Fructose.
Sources
- Crippen Method
- Crippen Method
- Aqueous biphasic systems composed of ionic liquid and fructose
- Boiling point of aqueous d-glucose and d-fructose solutions: Experimental determination and modeling with group-contribution method
- Solubility of monosaccharides in ionic liquids - Experimental data and modeling
- Conductivity in MnSO4-saccharide-water solutions at 298.15 K
- Acoustic investigation of choline chloride based ionic liquids analogues
- Solubility of glucose, xylose, fructose and galactose in ionic liquids: Experimental and theoretical studies using a continuum solvation model
- Osmotic properties of carbohydrate aqueous solutions
- Novel phase diagrams of aqueous two-phase systems based on tetrahydrofuran + carbohydrates + water: equilibrium data and partitioning experiments
- Thermodynamic studies on the phase equilibria of ternary {ionic liquid, 1-hexyl-3-methyl imidazolium chloride + D-fructose or sucrose + water} systems at 298.15 K and atmospheric pressure.
- Evaluation of the effect of ionic-liquids as soluting-out agents on the solubility of carbohydrates in aqueous solutions
- Efficient separation of curcumin using tetra butyl phosphonium bromide / carbohydrates (sorbitol, fructose) aqueous two-phase system
- Temperature dependence of the heat capacities in the solid state of 18 mono-, di-, and poly-saccharides
- Studies on volumetric properties of some saccharides in aqueous potassium chloride solutions over temperature range (288.15 to 318.15) K
- Effect of sodium acetate on the volumetric behaviour of some mono-, di-, and tri-saccharides in aqueous solutions over temperature range (288.15 to 318.15) K
- Viscometric studies on saccharides in aqueous magnesium chloride solutions at T = (288.15 to 318.15) K
- Apparent heat capacity measurements and thermodynamic functions of d(-)-fructose by standard and temperature-modulated calorimetry
- Influence of fructose on the diffusion of potassium hydrogen phosphate in aqueous solutions at 25 degC
- Study of interactions of D(+)-glucose and D(-)-fructose with trilithium citrate in aqueous medium through volumetric and ultrasonic properties over the temperature range T = (288.15 318.15) K
- Vapour-liquid equilibria for (water + ethanol + fructose): Experimental data and thermodynamic modelling
- Isopiestic determination of water activity and vapour pressure for ternary (ionic liquid, 1-hexyl-4-methyl pyridinium bromide + d-fructose or sucrose + water) systems and corresponding binary ionic liquid solutions at 298.15 K
- Studies on the interactions behaviour of polyhydroxy solutes D(+)-glucose and D(-)-fructose in aqueous triammonium citrate solutions over temperature range T = (288.15-318.15) K
- Effect of fruit and milk sugars on solute-solvent interactions of diphenhydramine-hydrochloride drug in aqueous solutions in viewpoint of volumetric and transport properties
- Volumetric and viscometric study of the ternary (dl-alanine/+d(-)-fructose + water) solution at different temperatures and atmospheric pressure
- Heat capacity and standard thermodynamic functions of three ketohexoses in monosaccharides including rare sugars: D-fructose, D-psicose, and D-tagatose
- Investigations on the temperature dependent volumetric and ultrasonic properties of structural isomers D(+)-glucose and D(-)-fructose in aqueous dipotassium oxalate solutions
- Solubility and solution thermodynamics of glucose and fructose in three asymmetrical dicationic ionic liquids from 323.15 K to 353.15 K
- Thermochemical behavior of 18-crown-6 in aqueous solutions of some monosaccharides
- Partial molar volumes, expansibilities and compressibilities of glyglyglycine in aqueous sucrose and fructose solutions between 288.15 to 308.15 K
- Fruit Sugar-based Deep Eutectic Solvents and their Physical Properties
- Application of the Eotvos and Guggenheim empirical rules for predicting the density and surface tension of ionic liquids analogues
- Study of solute-solute and solute-solvent interactions of N-acetyl glycine in aqueous D-fructose solutions at different temperatures
- Viscosities of Some Saccharides in Aqueous Solutions of Phosphate-Based Inorganic Salts
- Densities and Speeds of Sound of D(+)-Glucose, D(-)-Fructose, D(+)-Xylose and D(-)-Ribose in Aqueous Tripotassium Citrate Solutions at Different Temperatures
- Molar Heat Capacity of Selected Type III Deep Eutectic Solvents
- Volumetric and Acoustic Properties of Aqueous Carbohydrate Polymer Solutions
- Thermophysical Properties and Solubility of Different Sugar-Derived Molecules in Deep Eutectic Solvents
- Measurement and Correlation of Liquid Liquid Equilibria for the Ternary Systems of Water + d-Fructose + 1-Butanol, Water + d-Glucose + 1-Butanol, and Water + d-Galactose + 1-Butanol at (288.2, 303.2 and 318.2) K
- Salting-out Effect of Ionic Liquid, 1-Butyl-3-methyl Imidazolium Chloride on Aqueous d-Fructose or Sucrose Solutions at T = 298.15 K: Vapor-Liquid Equilibrium Study
- Extractions of Alkaloids Codeine and Caffeine with [Bmim][BF4]/Carbohydrate Aqueous Biphasic Systems as a Novel Class of Liquid-Liquid Extraction Systems
- Investigation of the Thermodynamic Properties in Aqueous Solutions Containing d-Fructose and Some Imidazolium-Based Ionic Liquids at Different Temperatures
- Measurements and Correlation of Water Activity in Aqueous Solutions Containing Diphenhydramine-Hydrochloride Drug, (D+)-Galactose, (D-)-Fructose, (D+)-Lactose, and Sucrose at 298.15 K
- Binary Mutual Diffusion Coefficients of Aqueous Solutions of Sucrose, Lactose, Glucose, and Fructose in the Temperature Range from (298.15 to 328.15) K
- Thermodynamic Study of Some Amino Acids, 2-Aminopropanoic Acid, 2-Amino-3-methylbutanoic Acid, 2-Amino-4-methylpentanoic Acid, and 2-Amino-3-phenylpropanoic Acid in Aqueous Saccharide Solutions at Different Temperatures: Volumetric and Ultrasonic Study
- Volumetric and Transport Behavior of Different Carbohydrates in Aqueous and Aqueous Urea Mixtures at Different Temperatures
- Volumetric and Viscometric Studies on Saccharide-Disodium Tetraborate (Borax) Interactions in Aqueous Solutions
- Fructose solubility in mixed (ethanol + water) solvent: experimental data and comparison among different thermodynamic models.
- Density of Mixtures Containing Sugars and Ionic Liquids: Experimental Data and PC-SAFT Modeling
- Studies on the Interactions of Saccharides and Methyl Glycosides with Lithium Chloride in Aqueous Solutions at (288.15 to 318.15) K
- Viscosity of Multicomponent Solutions of Simple and Complex Sugars in Water
- Joback Method
- McGowan Method
- NIST Webbook
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